RU2013122565A - POLYETHYLENE AND METHODS OF ITS PRODUCTION - Google Patents

POLYETHYLENE AND METHODS OF ITS PRODUCTION Download PDF

Info

Publication number
RU2013122565A
RU2013122565A RU2013122565/04A RU2013122565A RU2013122565A RU 2013122565 A RU2013122565 A RU 2013122565A RU 2013122565/04 A RU2013122565/04 A RU 2013122565/04A RU 2013122565 A RU2013122565 A RU 2013122565A RU 2013122565 A RU2013122565 A RU 2013122565A
Authority
RU
Russia
Prior art keywords
solution
methylaluminoxane
copolymer
trimethylaluminum
transition metal
Prior art date
Application number
RU2013122565/04A
Other languages
Russian (ru)
Other versions
RU2592276C2 (en
Inventor
Донна Дж. КРАУТЕР
Дейвид М. ФИСКУС
Original Assignee
Эксонмобил Кемикэл Пейтентс Инк.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from US12/909,412 external-priority patent/US8431661B2/en
Application filed by Эксонмобил Кемикэл Пейтентс Инк. filed Critical Эксонмобил Кемикэл Пейтентс Инк.
Publication of RU2013122565A publication Critical patent/RU2013122565A/en
Application granted granted Critical
Publication of RU2592276C2 publication Critical patent/RU2592276C2/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F210/16Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F10/02Ethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62Refractory metals or compounds thereof
    • C08F4/64Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/6592Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62Refractory metals or compounds thereof
    • C08F4/64Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/65916Component covered by group C08F4/64 containing a transition metal-carbon bond supported on a carrier, e.g. silica, MgCl2, polymer
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62Refractory metals or compounds thereof
    • C08F4/64Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/6592Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring
    • C08F4/65922Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring containing at least two cyclopentadienyl rings, fused or not
    • C08F4/65925Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring containing at least two cyclopentadienyl rings, fused or not two cyclopentadienyl rings being mutually non-bridged

Abstract

1. Способ полимеризации олефинов, включающий взаимодействие одного или большего количества олефинов с каталитической системой, содержащей металлоценовое соединение переходного металла и раствор метилалюмоксана, в способе количество триметилалюминия в растворе метилалюмоксана устанавливают равным от 1 до 25 мол.% или от 1 до 25 мас.% до использования в качестве активатора, где содержание триметилалюминия в мол.% или мас.% определяют с помощьюН ЯМР раствора до объединения с любой подложкой.2. Способ полимеризации олефинов, включающий взаимодействие одного или большего количества олефинов с каталитической системой, содержащей металлоценовое соединение переходного металла и раствор метилалюмоксана, и в этом способе количество неизвестных соединений, содержащихся в растворе метилалюмоксана, устанавливают равным от 0,10 до 0,65 интегральных единиц на основании пика триметилалюминия, нормированного на 3,0 интегральные единицы, до использования в качестве активатора, где неизвестные соединения идентифицируют, как третий сигнал вН ЯМР спектре раствора до объединения с любой подложкой в дополнение к сигналу, относящемуся к олигомерному метилалюмоксану, и сигналу, относящемуся к триметилалюминию, где указанные три сигнала, указанные в настоящем изобретении, не включают сигналов какого-либо растворителя.3. Способ по любому из пп.1 или 2, в котором количество триметилалюминия и количество неизвестных частиц регулируют путем добавления или удаления триметилалюминия, предпочтительно путем добавления или триметилалюминия в раствор метилалюмоксана или его удаления из раствора.4. Способ по любому из пп.1 или 2, в котором кат1. The method of polymerization of olefins, including the interaction of one or more olefins with a catalytic system containing a metallocene compound of a transition metal and a solution of methylaluminoxane, in the method the amount of trimethylaluminum in a solution of methylaluminoxane is set equal to from 1 to 25 mol.% Or from 1 to 25 wt.% before use as an activator, where the content of trimethylaluminum in mol.% or wt.% is determined using N NMR solution before combining with any substrate. 2. A method for the polymerization of olefins, comprising reacting one or more olefins with a catalyst system containing a metallocene transition metal compound and a methylaluminoxane solution, and in this method, the number of unknown compounds contained in the methylaluminoxane solution is set from 0.10 to 0.65 integral units per based on a trimethylaluminum peak normalized to 3.0 integral units, before being used as an activator, where unknown compounds are identified as the third signal in NMR spectrum of the solution prior to combining with any substrate in addition to the signal relating to the oligomeric methylaluminoxane and signals relating to trimethylaluminum, wherein said three signals mentioned in the present invention does not include any signal rastvoritelya.3. The method according to any one of claims 1 or 2, wherein the amount of trimethylaluminum and the amount of unknown particles are controlled by adding or removing trimethylaluminum, preferably by adding or trimethylaluminum to the solution of methylaluminoxane or removing it from the solution. The method according to any one of claims 1 or 2, wherein

Claims (15)

1. Способ полимеризации олефинов, включающий взаимодействие одного или большего количества олефинов с каталитической системой, содержащей металлоценовое соединение переходного металла и раствор метилалюмоксана, в способе количество триметилалюминия в растворе метилалюмоксана устанавливают равным от 1 до 25 мол.% или от 1 до 25 мас.% до использования в качестве активатора, где содержание триметилалюминия в мол.% или мас.% определяют с помощью 1Н ЯМР раствора до объединения с любой подложкой.1. The method of polymerization of olefins, including the interaction of one or more olefins with a catalytic system containing a metallocene compound of a transition metal and a solution of methylaluminoxane, in the method the amount of trimethylaluminum in a solution of methylaluminoxane is set equal to from 1 to 25 mol.% Or from 1 to 25 wt.% before use as an activator, where the content of trimethylaluminum in mol.% or wt.% is determined using 1 H NMR solution before combining with any substrate. 2. Способ полимеризации олефинов, включающий взаимодействие одного или большего количества олефинов с каталитической системой, содержащей металлоценовое соединение переходного металла и раствор метилалюмоксана, и в этом способе количество неизвестных соединений, содержащихся в растворе метилалюмоксана, устанавливают равным от 0,10 до 0,65 интегральных единиц на основании пика триметилалюминия, нормированного на 3,0 интегральные единицы, до использования в качестве активатора, где неизвестные соединения идентифицируют, как третий сигнал в 1Н ЯМР спектре раствора до объединения с любой подложкой в дополнение к сигналу, относящемуся к олигомерному метилалюмоксану, и сигналу, относящемуся к триметилалюминию, где указанные три сигнала, указанные в настоящем изобретении, не включают сигналов какого-либо растворителя.2. A method for the polymerization of olefins, comprising reacting one or more olefins with a catalyst system containing a metallocene transition metal compound and a methylaluminoxane solution, and in this method, the number of unknown compounds contained in the methylaluminoxane solution is set to be from 0.10 to 0.65 integral units based on a peak of trimethylaluminum normalized to 3.0 integral units before being used as an activator, where unknown compounds are identified as the third signal in the 1 H NMR spectrum of the solution prior to combining with any substrate in addition to the signal related to oligomeric methylaluminoxane and the signal related to trimethylaluminum, where the three signals indicated in the present invention do not include signals of any solvent. 3. Способ по любому из пп.1 или 2, в котором количество триметилалюминия и количество неизвестных частиц регулируют путем добавления или удаления триметилалюминия, предпочтительно путем добавления или триметилалюминия в раствор метилалюмоксана или его удаления из раствора.3. The method according to any one of claims 1 or 2, in which the amount of trimethylaluminum and the number of unknown particles are controlled by adding or removing trimethylaluminum, preferably by adding or trimethylaluminum to the solution of methylaluminoxane or removing it from the solution. 4. Способ по любому из пп.1 или 2, в котором каталитическая система в растворе метилалюмоксана до объединения с любой подложкой характеризуется отношением количества молей алюминия к количеству молей переходного металла (предпочтительно отношением количества молей алюминия к количеству молей гафния), составляющим 175:1 или менее.4. The method according to any one of claims 1 or 2, in which the catalytic system in a solution of methylaluminoxane prior to combining with any substrate is characterized by the ratio of the number of moles of aluminum to the number of moles of transition metal (preferably the ratio of the number of moles of aluminum to the number of moles of hafnium) of 175: 1 or less. 5. Способ по любому из пп.1 или 2, в котором металлоценовое соединение переходного металла описывается формулой:5. The method according to any one of claims 1 or 2, in which the metallocene transition metal compound is described by the formula: CpACpBHfX∗n Cp A Cp B HfX ∗ n в которой каждый X∗ и каждая группа Cp химически связана с Hf, n равно 1 или 2, CpA и CB могут быть одинаковыми или разными циклопентадиенильными лигандами или лигандами, изолобальными по отношению к циклопентадиенилу, любой из которых или оба могут содержать гетероатомы и любой из которых или оба могут быть замещенными, и где способ предпочтительно является газофазным способом.in which each X ∗ and each Cp group is chemically bonded to Hf, n is 1 or 2, Cp A and C B can be the same or different cyclopentadienyl ligands or ligands, isobalic to cyclopentadienyl, either of which can contain heteroatoms and either of which or both may be substituted, and where the method is preferably a gas phase method. 6. Способ влияния на меж- и/или внутримолекулярное распределение сомономера и/или молекулярно-массовое распределение в сополимере путем регулирования количества триметилалюминия в каталитической системе, использующейся в способе полимеризации, каталитическая система включает раствор метилалюмоксана и металлоценовое соединение переходного металла.6. A method for influencing the inter- and / or intramolecular distribution of the comonomer and / or molecular weight distribution in the copolymer by controlling the amount of trimethylaluminium in the catalyst system used in the polymerization method, the catalyst system includes a methylaluminoxane solution and a transition metal metallocene compound. 7. Способ по п.6, в котором в сополимере содержание триады ([ННН]) сомономера увеличивают и/или молекулярно-массовое распределение уменьшают путем уменьшения количества триметилалюминия в каталитической системе, содержащей раствор метилалюмоксана и металлоценовое соединение переходного металла, где Е означает образованное из этилена звено и H означает образованное из сомономера звено в сополимере.7. The method according to claim 6, in which in the copolymer the content of the triad ([IUU]) of the comonomer is increased and / or the molecular weight distribution is reduced by reducing the amount of trimethylaluminum in a catalyst system containing a solution of methylaluminoxane and a metallocene transition metal compound, where E means formed from ethylene, and H means a unit formed from a comonomer in a copolymer. 8. Способ улучшения рабочих характеристик пленки, предпочтительно сопротивления раздиру и/или ударопрочности пленки, изготовленной из сополимера этилена, путем уменьшения количества триметилалюминия в каталитической системе, использующейся в способе полимеризации, каталитическая система включает раствор метилалюмоксана и металлоценовое соединение переходного металла.8. A method for improving film performance, preferably tear resistance and / or impact resistance of a film made from an ethylene copolymer by reducing the amount of trimethylaluminium in the catalyst system used in the polymerization method, the catalyst system includes a methylaluminoxane solution and a transition metal metallocene compound. 9. Способ по любому из пп.6-8, в котором способом полимеризации является непрерывным способ, предпочтительно газофазный способ, и количества триметилалюминия регулируют в реальном масштабе времени до поступления в реактор полимеризации.9. The method according to any one of claims 6 to 8, in which the polymerization method is a continuous method, preferably a gas phase method, and the amounts of trimethylaluminium are adjusted in real time before entering the polymerization reactor. 10. Способ мониторинга количества триметилалюминия в каталитической системе, использующейся в способе полимеризации, каталитическая система включает раствор метилалюмоксана и металлоценовое соединение переходного металла, путем мониторинга интенсивности (посредством интегральных единиц) сигнала 1Н ЯМР неизвестных частиц, содержащихся в растворе метилалюмоксана, и этот сигнал является третьим сигналом в 1Н ЯМР спектре раствора до объединения с любой подложкой в дополнение к сигналу, относящемуся к олигомерному метилалюмоксану, и сигналу, относящемуся к триметилалюминию, где указанные три сигнала, указанные в настоящем изобретении, не включают сигналов какого-либо растворителя.10. A method for monitoring the amount of trimethylaluminium in the catalyst system used in the polymerization method, the catalyst system includes a methylaluminoxane solution and a transition metal metallocene compound by monitoring the intensity (by integral units) of the 1 H NMR signal of unknown particles contained in the methylaluminoxane solution, and this signal is the third signal in the 1 H NMR spectrum of the solution prior to combining with any substrate in addition to the signal related to oligomeric methylaluminoxane and nalum related to trimethylaluminum, where the three signals indicated in the present invention do not include the signals of any solvent. 11. Сополимер, полученный способом по любому из пп.1-5 или способом по любому из пп.6-9.11. The copolymer obtained by the method according to any one of claims 1 to 5 or by the method according to any one of claims 6 to 9. 12. Сополимер по п.11, которым является сополимер, содержащий этилен и от 0,5 до 25 мол.% C3-C20-олефинового сомономера, указанный сополимер обладает следующими характеристиками: растягивающее напряжение при вторичном пределе текучести, равное 12 МПа или более; отношение предельного относительного удлинения к разрывному напряжению, равное 20 или более; растягивающее напряжение при удлинении на 200% (МПа), которое больше, чем растягивающее напряжение при вторичном пределе текучести (МПа); содержание триад сомономера (триад [ННН]), равное 0,0005 мол.% или более; плотность, равная 0,910 г/см3 или более, и 1% секущий модуль упругости, равный от 30 до 100 МПа.12. The copolymer according to claim 11, which is a copolymer containing ethylene and from 0.5 to 25 mol% of a C 3 -C 20 olefin comonomer, said copolymer has the following characteristics: tensile stress at a secondary yield strength of 12 MPa or more; a ratio of ultimate elongation to tensile stress of 20 or more; tensile stress at elongation of 200% (MPa), which is greater than tensile stress at a secondary yield strength (MPa); the content of triads of comonomer (triads [IUU]) equal to 0.0005 mol.% or more; a density of 0.910 g / cm 3 or more, and a 1% secant modulus of elasticity, equal to 30 to 100 MPa. 13. Сополимер по любому из пп.11 или 12, в котором отклонение от статистического, если статистическое значение мольной доли [ННН] в сополимере вычитают из измеренного значения мольной доли [ННН], больше 0, и/или отклонение от статистического, если статистическое значение мольной доли [ЕНЕ] в сополимере вычитают из измеренного значения мольной доли [ЕНЕ], больше 0.13. The copolymer according to any one of paragraphs.11 or 12, in which the deviation from the statistical, if the statistical value of the molar fraction [IUU] in the copolymer is subtracted from the measured value of the molar fraction [IUU], is greater than 0, and / or the deviation from the statistical if statistical the molar fraction [ENE] in the copolymer is subtracted from the measured molar fraction [ENE], greater than 0. 14. Сополимер по любому из пп.11 или 12, где полимер обладает пределом прочности при растяжении при пределе текучести, равным более 11 МПа, и/или предельным удлинением, равным более 750%, и/или предельным напряжением, равным менее 40 МПа, и/или отношением предельной деформации к предельному напряжению, равным более 17, и/или 1% секущим модулем упругости, равным от 30 до 100 МПа, и/или характеристическим раздиром, равным 300 г/мил или менее.14. The copolymer according to any one of paragraphs.11 or 12, where the polymer has a tensile strength at a yield strength of more than 11 MPa, and / or an ultimate elongation of more than 750%, and / or an ultimate stress of less than 40 MPa, and / or the ratio of ultimate strain to ultimate stress equal to more than 17, and / or 1% secant modulus of elasticity, equal to from 30 to 100 MPa, and / or characteristic shear, equal to 300 g / mil or less. 15. Сополимер этилена с C4-C8-альфа-олефином, содержащий от 0,5 до 25 мол.% сомономера и обладающий плотностью, равной 0,910 г/см или более, в котором отклонение от статистического, если рассчитанное статистическое значение мольной доли [ННН] в сополимере вычитают из измеренного значения мольной доли [ННН], больше 0, и/или отклонение от статистического, если рассчитанное статистическое значение мольной доли [ЕНЕ] в сополимере вычитают из измеренного значения мольной доли [ЕНЕ], больше 0, где Е означает звено, образованное из этилена, и H означает звено, образованное из C4-C8-альфа-олефинового сомономера, в сополимере. 15. A copolymer of ethylene with a C 4 -C 8 alpha-olefin, containing from 0.5 to 25 mol.% Comonomer and having a density equal to 0.910 g / cm or more, in which the deviation from the statistical if the calculated statistical value of the mole fraction [IUU] in the copolymer is subtracted from the measured mole fraction [IUU], greater than 0, and / or a deviation from the statistical if the calculated statistical mole fraction [ENE] in the copolymer is subtracted from the measured mole fraction [ENE], more than 0, where E means a unit formed from ethylene, and H means a unit, formed from a C 4 -C 8 alpha olefin comonomer in a copolymer.
RU2013122565/04A 2010-10-21 2011-10-14 Polyethylene and methods for production thereof RU2592276C2 (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
US12/909,412 2010-10-21
US12/909,412 US8431661B2 (en) 2010-10-21 2010-10-21 Polyethylene and process for production thereof
EP10194265.4 2010-12-09
EP10194265 2010-12-09
PCT/US2011/056336 WO2012096698A2 (en) 2010-10-21 2011-10-14 Polyethylene and process for production thereof

Publications (2)

Publication Number Publication Date
RU2013122565A true RU2013122565A (en) 2014-11-27
RU2592276C2 RU2592276C2 (en) 2016-07-20

Family

ID=46507614

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2013122565/04A RU2592276C2 (en) 2010-10-21 2011-10-14 Polyethylene and methods for production thereof

Country Status (5)

Country Link
EP (2) EP2915826B1 (en)
KR (2) KR101821026B1 (en)
CN (1) CN103261239B (en)
RU (1) RU2592276C2 (en)
WO (1) WO2012096698A2 (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2970610A2 (en) * 2013-03-15 2016-01-20 Univation Technologies, LLC Hafnocene catalyzed polyethylene films having rapid cling development
KR101721194B1 (en) 2013-11-28 2017-03-29 주식회사 엘지화학 Method for preparing supported metallocene catalyst
WO2017054398A1 (en) 2015-09-28 2017-04-06 中国石油天然气股份有限公司 Spherical supported transition metal catalyst
KR101889598B1 (en) 2015-12-08 2018-08-17 주식회사 엘지화학 Olefin based polymer
KR20190112293A (en) * 2017-02-20 2019-10-04 엑손모빌 케미칼 패턴츠 인코포레이티드 Group 4 catalyst compound and method of using the same
EP3807358B1 (en) 2018-06-13 2023-11-15 ExxonMobil Chemical Patents Inc. Polyolefin blend compositions
CN109521041B (en) * 2018-11-30 2022-05-17 华南理工大学 XLPE material thermal aging dynamic process multiphase combined detection method
KR102251553B1 (en) * 2020-02-20 2021-05-13 한국정상화성 주식회사 Manufacturing method of packing member for prefab water-tank
CN112285048A (en) * 2020-10-29 2021-01-29 广东电网有限责任公司电力科学研究院 Method and system for representing insulation aging state of crosslinked polyethylene cable

Family Cites Families (65)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3248179A (en) 1962-02-26 1966-04-26 Phillips Petroleum Co Method and apparatus for the production of solid polymers of olefins
US4543399A (en) 1982-03-24 1985-09-24 Union Carbide Corporation Fluidized bed reaction systems
US4588790A (en) 1982-03-24 1986-05-13 Union Carbide Corporation Method for fluidized bed polymerization
US4613484A (en) 1984-11-30 1986-09-23 Phillips Petroleum Company Loop reactor settling leg system for separation of solid polymers and liquid diluent
US4665208A (en) 1985-07-11 1987-05-12 Exxon Chemical Patents Inc. Process for the preparation of alumoxanes
ATE114678T1 (en) 1986-09-24 1994-12-15 Mitsui Petrochemical Ind PROCESSES FOR POLYMERIZATION OF POLYOLEFINS.
JPH0780933B2 (en) 1986-11-20 1995-08-30 三井石油化学工業株式会社 Olefin Polymerization Method
US5198401A (en) 1987-01-30 1993-03-30 Exxon Chemical Patents Inc. Ionic metallocene catalyst compositions
JPH0742301B2 (en) 1987-02-14 1995-05-10 三井石油化学工業株式会社 Particulate aluminoxane, its manufacturing method and its use
JP2538588B2 (en) 1987-04-03 1996-09-25 三井石油化学工業株式会社 Method for producing solid catalyst for olefin polymerization
US5206199A (en) 1987-04-20 1993-04-27 Mitsui Petrochemical Industries, Ltd. Catalyst for polymerizing an olefin and process for polymerizing an olefin
FR2634212B1 (en) 1988-07-15 1991-04-19 Bp Chimie Sa APPARATUS AND METHOD FOR POLYMERIZATION OF GASEOUS OLEFINS IN A FLUIDIZED BED REACTOR
US5091352A (en) 1988-09-14 1992-02-25 Mitsui Petrochemical Industries, Ltd. Olefin polymerization catalyst component, olefin polymerization catalyst and process for the polymerization of olefins
US5041584A (en) 1988-12-02 1991-08-20 Texas Alkyls, Inc. Modified methylaluminoxane
US4908463A (en) 1988-12-05 1990-03-13 Ethyl Corporation Aluminoxane process
US5103031A (en) 1989-02-21 1992-04-07 Ethyl Corporation Falling film aluminoxane process
US4968827A (en) 1989-06-06 1990-11-06 Ethyl Corporation Alkylaluminoxane process
US4924018A (en) 1989-06-26 1990-05-08 Ethyl Corporation Alkylaluminoxane process
US5157137A (en) 1991-07-26 1992-10-20 Ethyl Corporation Method of making gel free alkylaluminoxane solutions
US5308815A (en) 1991-07-26 1994-05-03 Ethyl Corporation Heterogeneous methylaluminoxane catalyst system
US5235081A (en) 1992-03-18 1993-08-10 Ethyl Corporation Method of removing gel forming materials from methylaluminoxanes
CA2124187C (en) 1991-11-25 2001-08-07 Howard William Turner Polyonic transition metal catalyst composition
US5329032A (en) 1992-03-18 1994-07-12 Akzo Chemicals Inc. Polymethylaluminoxane of enhanced solution stability
US5436304A (en) 1992-03-19 1995-07-25 Exxon Chemical Patents Inc. Process for polymerizing monomers in fluidized beds
US5352749A (en) 1992-03-19 1994-10-04 Exxon Chemical Patents, Inc. Process for polymerizing monomers in fluidized beds
US5248801A (en) 1992-08-27 1993-09-28 Ethyl Corporation Preparation of methylaluminoxanes
US5317036A (en) 1992-10-16 1994-05-31 Union Carbide Chemicals & Plastics Technology Corporation Gas phase polymerization reactions utilizing soluble unsupported catalysts
US5939346A (en) 1992-11-02 1999-08-17 Akzo Nobel N.V. Catalyst system comprising an aryloxyaluminoxane containing an electron withdrawing group
US5391793A (en) 1992-11-02 1995-02-21 Akzo Nobel N.V. Aryloxyaluminoxanes
US5391529A (en) 1993-02-01 1995-02-21 Albemarle Corporation Siloxy-aluminoxane compositions, and catalysts which include such compositions with a metallocene
US5462999A (en) 1993-04-26 1995-10-31 Exxon Chemical Patents Inc. Process for polymerizing monomers in fluidized beds
WO1994025495A1 (en) 1993-05-20 1994-11-10 Exxon Chemical Patents Inc. Process for polymerizing monomers in fluidized beds
ZA943399B (en) 1993-05-20 1995-11-17 Bp Chem Int Ltd Polymerisation process
US5453471B1 (en) 1994-08-02 1999-02-09 Carbide Chemicals & Plastics T Gas phase polymerization process
US5643847A (en) 1994-08-03 1997-07-01 Exxon Chemical Patents Inc. Supported ionic catalyst composition
US5763543A (en) 1994-09-14 1998-06-09 Exxon Chemical Patents Inc. Olefin polymerization process with little or no scavenger present
US5616661A (en) 1995-03-31 1997-04-01 Union Carbide Chemicals & Plastics Technology Corporation Process for controlling particle growth during production of sticky polymers
US5869723A (en) 1995-06-08 1999-02-09 Showa Denko K.K. Ionic compound and olefin polymerization catalyst containing the same
US5731253A (en) 1995-07-27 1998-03-24 Albemarle Corporation Hydrocarbylsilloxy - aluminoxane compositions
US5693838A (en) 1995-11-13 1997-12-02 Albemarle Corporation Aluminoxane process and product
US5856256A (en) 1996-02-20 1999-01-05 Northwestern University Organo-Lewis acid as cocatalyst for cationic homogeneous Ziegler-Natta olefin polymerizations
US6034024A (en) * 1996-05-10 2000-03-07 Albemarle Corporation Heat treated alumoxanes
US5731451A (en) 1996-07-12 1998-03-24 Akzo Nobel Nv Modified polyalkylauminoxane composition formed using reagent containing aluminum trialkyl siloxide
ATE325821T1 (en) 1996-08-13 2006-06-15 Basell Polyolefine Gmbh SUPPORTED CHEMICAL COMPOUND
US5854166A (en) 1996-08-19 1998-12-29 Northwestern University Synthesis and use of (perfluoroaryl) fluoro-aluminate anion
US5847177A (en) 1996-10-10 1998-12-08 Albemarle Corporation Production of hydrocarbon-soluble hydrocarbylaluminoxanes
US5744656A (en) 1996-10-25 1998-04-28 Boulder Scientific Company Conversion of hexafluorobenzene to bromopentafluorobenzene
JP2001517714A (en) 1997-09-19 2001-10-09 ザ ダウ ケミカル カンパニー Modified aluminoxane catalyst activator
US6242545B1 (en) 1997-12-08 2001-06-05 Univation Technologies Polymerization catalyst systems comprising substituted hafinocenes
US6040261A (en) 1999-04-15 2000-03-21 Equistar Chemicals, Lp Supported single-site catalyst and olefin polymerization process
SK5492002A3 (en) 1999-10-22 2002-12-03 Univation Tech Llc Start up methods for multiple catalyst systems
US6399722B1 (en) 1999-12-01 2002-06-04 Univation Technologies, Llc Solution feed of multiple catalysts
US6444833B1 (en) * 1999-12-15 2002-09-03 Basell Technology Company Bv Metallocene compounds, process for their preparation and their use in catalytic systems for the polymerization of olefins
US6956088B2 (en) 2001-07-19 2005-10-18 Univation Technologies, Llc Polyethylene films with improved physical properties
US6936675B2 (en) 2001-07-19 2005-08-30 Univation Technologies, Llc High tear films from hafnocene catalyzed polyethylenes
US7265193B2 (en) 2003-01-31 2007-09-04 Exxonmobil Chemical Patents Inc. Polymerization process
WO2004108775A1 (en) 2003-06-05 2004-12-16 Dow Global Technologies Inc. Activated multinuclear transition metal catalyst compositions
US7244795B2 (en) * 2003-12-08 2007-07-17 Univation Technologies, Llc Polymerization process using metallocene catalyst systems
US7276567B2 (en) 2004-04-16 2007-10-02 Exxonmobil Chemical Patents Inc. Heterocyclic substituted metallocene compounds for olefin polymerization
US7157531B2 (en) * 2004-06-21 2007-01-02 Univation Technologies, Llc Methods for producing polymers with control over composition distribution
DE602005010255D1 (en) * 2004-07-08 2008-11-20 Exxonmobil Chem Patents Inc CATALYST SYSTEM FOR OLEFIN POLYMERIZATION AND METHOD FOR ITS USE
EP1650231A1 (en) 2004-10-21 2006-04-26 Total Petrochemicals Research Feluy Polyolefins prepared from a metallocene and a new single site catalyst components in a single reactor
US8247065B2 (en) 2006-05-31 2012-08-21 Exxonmobil Chemical Patents Inc. Linear polymers, polymer blends, and articles made therefrom
US20090297810A1 (en) 2008-05-30 2009-12-03 Fiscus David M Polyethylene Films and Process for Production Thereof
WO2009082546A2 (en) * 2007-12-18 2009-07-02 Exxonmobil Chemical Patents Inc. Polyethylene films and process for production thereof

Also Published As

Publication number Publication date
EP2630168A4 (en) 2014-10-29
EP2915826B1 (en) 2024-02-28
WO2012096698A3 (en) 2012-09-20
EP2630168A2 (en) 2013-08-28
KR20150083927A (en) 2015-07-20
KR20130113470A (en) 2013-10-15
CN103261239B (en) 2016-04-06
RU2592276C2 (en) 2016-07-20
CN103261239A (en) 2013-08-21
WO2012096698A2 (en) 2012-07-19
EP2915826A1 (en) 2015-09-09
KR101821026B1 (en) 2018-01-22

Similar Documents

Publication Publication Date Title
RU2013122565A (en) POLYETHYLENE AND METHODS OF ITS PRODUCTION
US11572461B2 (en) Multimodal copolymer of ethylene and at least two alpha-olefin comonomers and final articles made thereof
US9266910B2 (en) Asymmetric polypropylene catalysts
KR101395970B1 (en) High temperature polyethylene solution polymerization process
US20180346618A1 (en) Long Chain Branched Polypropylene
RU2018107540A (en) METALCENE DOUBLE CATALYTIC SYSTEMS ZIGLER-NATT WITH ACTIVATORS-CARRIERS
EP2935297B1 (en) Bridged metallocene compounds, catalyst systems and processes for polymerization therewith
US20140179884A1 (en) Bridged Metallocene Compounds, Catalyst Systems and Processes for Polymerization Therewith
RU2010153869A (en) METHOD FOR PRODUCING BIMODAL POLYETHYLENE AND PRODUCTS FROM IT
RU2009136640A (en) METHOD FOR POLYMERIZATION OF OLEFINS
KR20180041116A (en) Multimodal polyethylene copolymer
JP6466566B2 (en) Method for producing polyolefin polymer for fiber production
KR20090040309A (en) Butene-1 copolymers
EP3063184A1 (en) Asymmetric polypropylene catalysts
CN114269798A (en) High propylene content EP with low glass transition temperature
KR20130046408A (en) Polyolefin with multi-modal molecular weight distributions and pipe comprising the same
JP6458137B2 (en) Polyolefin pellets for fiber production and fibers containing the same
US20180305534A1 (en) Methods for Making Polypropylene and Compositions Made Thereby
EP1448633B1 (en) Two-step polymerization process
KR101299650B1 (en) Polyolefin with multi-modal molecular weight distributions and preparation method thereof
US8877880B2 (en) Method for controlling polyolefin properties
EP3398976A1 (en) Hybrid supported metallocene catalyst, method for preparing olefin polymer by using same, and olefin polymer having improved melt strength
US20050288463A1 (en) Olefin polymerization process in the presence of a radical generating system
EP3621996B1 (en) Catalyst systems and processes for using the same
JP2015524854A (en) Free radical process for making ethylene-based polymers using alkylated phenols

Legal Events

Date Code Title Description
HZ9A Changing address for correspondence with an applicant